artículo académico

• BAROTROPIC PHENOMENA IN BINARY MIXTURES.  FLUID PHASE EQUILIBRIA.  394:175-185. 2015
• JOURNAL OF CHEMICAL AND ENGINEERING DATA.  JOURNAL OF CHEMICAL AND ENGINEERING DATA.  60(12):3766-3775. 2015
• COMPREHENSIVE CHARACTERIZATION OF INTERFACIAL BEHAVIOR FOR THE MIXTURE CO2 + H2O + CH4: COMPARISON BETWEEN ATOMISTIC AND COARSE GRAINED MOLECULAR SIMULATION MODELS AND DENSITY GRADIENT THEORY.  JOURNAL OF PHYSICAL CHEMISTRY C.  118:24504-24519. 2014
• EXPERIMENTAL DETERMINATION AND THEORETICAL PREDICTION OF THE VAPOR-LIQUID EQUILIBRIUM AND INTERFACIAL TENSIONS OF THE SYSTEM METHYL-TERT-BUTYL ETHER+2,5-DIMETHYLFURAN.  FUEL.  116:183-190. 2014
• FLUID PHASE EQUILIBRIA.  FLUID PHASE EQUILIBRIA.  361:229-236. 2014
• FLUID PHASE EQUILIBRIA.  FLUID PHASE EQUILIBRIA.  380:82-92. 2014
• FUEL.  FUEL.  117:996-1003. 2014
• HIGH-PRESSURE INTERFACIAL TENSIONS FOR NITROGEN PLUS ETHANOL, OR HEXANE OR 2-METHOXY-2-METHYLBUTANE: A COMPARISON BETWEEN EXPERIMENTAL TENSIOMETRY AND MONTE CARLO SIMULATIONS.  JOURNAL OF SUPERCRITICAL FLUIDS.  89:78-88. 2014
• JOURNAL CHEMICAL & ENGINEERING DATA 2014
• JOURNAL OF CHEMICAL PHYSICS.  JOURNAL OF CHEMICAL PHYSICS.  141:1-12. 2014
• COARSE-GRAINED MOLECULAR DYNAMIC SIMULATIONS OF SELECTED THERMOPHYSICAL PROPERTIES FOR 1-BUTYL-3-METHYLIMIDAZOLIUM HEXAFLUOROPHOSPHATE.  JOURNAL OF MOLECULAR LIQUIDS.  186:106-115. 2013
• DYNAMIC MODELING AND SIMULATION OF AN ALEMBIC PEAR WINE DISTILLATION.  FOOD AND BIOPRODUCTS PROCESSING.  91(c4):447-456. 2013
• EXPERIMENTAL DETERMINATION AND THEORETICAL MODELING OF THE VAPOR-LIQUID EQUILIBRIUM AND DENSITIES OF THE BINARY SYSTEM BUTAN-2-OL + TETRAHYDRO-2H-PYRAN.  FLUID PHASE EQUILIBRIA.  342:52-59. 2013
• EXPERIMENTAL DETERMINATION AND THEORETICAL PREDICTION OF THE VAPOR-LIQUID EQUILIBRIUM AND INTERFACIAL TENSIONS OF THE SYSTEM METHYL-TERT-BUTYL ETHER+2,5-DIMETHYLFURAN.  FUEL.  116:183-190. 2013
• FLUID PHASE EQUILIBRIA.  FLUID PHASE EQUILIBRIA.  345:60-67. 2013
• ISOBARIC VAPOR-LIQUID EQUILIBRIUM AND ISOTHERMAL INTERFACIAL TENSIONS FOR THE SYSTEM ETHANOL+2,5-DIMETHYLFURAN.  JOURNAL OF CHEMICAL AND ENGINEERING DATA.  58(11):3226-3232. 2013
• JOURNAL OF CHEMICAL AND ENGINEERING DATA.  JOURNAL OF CHEMICAL AND ENGINEERING DATA.  58:1203-1211. 2013
• EXPERIMENTAL DETERMINATION AND THEORETICAL MODELING OF THE VAPOR-LIQUID EQUILIBRIUM AND SURFACE TENSIONS OF HEXANE + TETRAHYDRO-2H-PYRAN .  FLUID PHASE EQUILIBRIA.  316:55-65. 2012
• JOURNAL OF CHEMICAL AND ENGINEERING DATA.  JOURNAL OF CHEMICAL AND ENGINEERING DATA.  57:561-567. 2012
• JOURNAL OF CHEMICAL AND ENGINEERING DATA.  JOURNAL OF CHEMICAL AND ENGINEERING DATA.  57:2681-2688. 2012
• FLUID PHASE EQUILIBRIA.  FLUID PHASE EQUILIBRIA.  54:137-147. 2011
• FLUID PHASE EQUILIBRIA.  FLUID PHASE EQUILIBRIA.  308:15-24. 2011
• INTERFACIAL TENSIONS OF BINARY MIXTURES OF ETHANOL WITH OCTANE, DECANE, DODECANE, AND TETRADECANE.  JOURNAL OF CHEMICAL THERMODYNAMICS.  43:1395-1400. 2011
• JOURNAL OF CHEMICAL AND ENGINEERING DATA.  JOURNAL OF CHEMICAL AND ENGINEERING DATA.  56:2256-2265. 2011
• JOURNAL OF CHEMICAL AND ENGINEERING DATA.  JOURNAL OF CHEMICAL AND ENGINEERING DATA.  56:3142-3148. 2011
• JOURNAL OF CHEMICAL AND ENGINEERING DATA.  JOURNAL OF CHEMICAL AND ENGINEERING DATA.  55:428-434. 2010
• COMMENTS ON "EXPERIMENTAL ISOBARIC VAPOR-LIQUID EQUILIBRIUM DATA FOR BINARY MIXTURES OF CYCLIC ETHERS WITH (1-METHYLETHYL)BENZENE" (GILL, B.K.; RATTAN, V.K.; KAPOOR, S. J. J. CHEM. ENG. DATA 2008, 53, 2041-2043.  JOURNAL OF CHEMICAL AND ENGINEERING DATA.  54:1165-1167. 2009
• COMMENTS ON "JOULE-THOMSON INVERSION CURVES AND THIRD VIRIAL COEFFICIENTS FOR PURE FLUIDS FROM MOLECULAR-BASED MODELS" AND PREDICTED INVERSION CURVE AND THIRD VIRIAL COEFFICIENTS OF CARBON DIOXIDE AT HIGH TEMPERATURES.  INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH.  48:6901-6903. 2009
• FLUID PHASE EQUILIBRIA.  FLUID PHASE EQUILIBRIA.  277(2):121-125. 2009
• JOURNAL OF SUPERCRITICAL FLUIDS.  JOURNAL OF SUPERCRITICAL FLUIDS.  48(2):108-119. 2009
• A NEW REFERENCE STATE FOR THE CALCULATION OF ACTIVITY COEFFICIENTS: COMMENT ON THE PAPER "A MOLECULAR THEORY OF THE ACTIVITY COEFFICIENT AND THEIR REFERENCE FUGACITIES AT THE SUPERCRITICAL STATE.  INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH.  47:5758-5760. 2008
• AN ACCURATE DIRECT TECHNIQUE FOR PARAMETERIZING CUBIC EQUATIONS OF STATE. PART I. DETERMINING THE COHESION TEMPERATURE FUNCTION IN THE LOW TEMPERATURE RANGE.  FLUID PHASE EQUILIBRIA.  265:63-83. 2008
• AN ACCURATE DIRECT TECHNIQUE FOR PARAMETERIZING CUBIC EQUATIONS OF STATE. PART II. SPECIALIZING MODELS FOR PREDICTING VAPOR PRESSURES AND PHASE DENSITIES.  FLUID PHASE EQUILIBRIA.  265:155-172. 2008
• AN ACCURATE DIRECT TECHNIQUE FOR PARAMETERIZING CUBIC EQUATIONS OF STATE. PART III. APPLICATION OF A CROSSOVER TREATMENT.  FLUID PHASE EQUILIBRIA.  264:201-210. 2008
• FLUID PHASE EQUILIBRIA.  FLUID PHASE EQUILIBRIA.  270:75-86. 2008
• FLUID PHASE EQUILIBRIA.  FLUID PHASE EQUILIBRIA.  273:68-77. 2008
• PHYSICS AND CHEMISTRY OF LIQUIDS.  PHYSICS AND CHEMISTRY OF LIQUIDS.  46:185-200. 2008
• AZEOTROPIC BEHAVIOR OF DIETERICI BINARY FLUIDS.  FLUID PHASE EQUILIBRIA.  257:18-26. 2007
• FLUID PHASE EQUILIBRIA.  FLUID PHASE EQUILIBRIA.  255:121-130. 2007
• INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH.  INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH.  46:947-954. 2007
• ASSOCIATION AND MOLECULAR CHAIN LENGTH EFFECTS ON INTERFACIAL BEHAVIOUR.  PHYSICS AND CHEMISTRY OF LIQUIDS.  44:45-59. 2006
• COMMENTS ON "COMPUTING ALL THE AZEOTROPES IN REFRIGERANT MIXTURES THROUGH EQUATIONS OF STATE" BY NAVEED ASLAM AND AYDIN K. SUNOL (FLUID PHASE EQUILIB. 2004, 224, 97-109).  FLUID PHASE EQUILIBRIA.  235:232-237. 2005
• CORRELATION AND PREDICTION OF INTERFACE TENSION FOR FLUID MIXTURES: AN APPROACH BASED ON CUBIC EQUATIONS OF STATE WITH THE WONG-SANDLER MIXING RULE.  JOURNAL OF PHASE EQUILIBRIA.  26(3):215-224. 2005
• FLUID PHASE EQUILIBRIA.  FLUID PHASE EQUILIBRIA.  227:225-238. 2005
• INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH.  INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH.  44(7):2292-2300. 2005
• INTERNATIONAL JOURNAL OF THERMOPHYSICS.  INTERNATIONAL JOURNAL OF THERMOPHYSICS.  26(1):13-29. 2005
• JOURNAL OF CHEMICAL PHYSICS.  JOURNAL OF CHEMICAL PHYSICS.  123:034505-1-034505-10. 2005
• CHEMICAL ENGINEERING SCIENCE.  CHEMICAL ENGINEERING SCIENCE.  59(3):633-643. 2004
• ESTIMATION OF INTERFACIAL BEHAVIOR USING THE GLOBAL PHASE DIAGRAM APPROACH: I. CARBON DIOXIDE-N-ALKANES.  THERMOCHIMICA ACTA.  411:171-176. 2004
• ESTIMATION OF LIQUID-LIQUID-VAPOR EQUILIBRIA IN BINARY MIXTURES OF N-ALKANES.  INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH.  43:5957-5964. 2004
• GLOBAL PHASE DIAGRAM ANALYSIS OF THE DIETERICI EQUATION OF STATE.  PHYSICAL CHEMISTRY CHEMICAL PHYSICS.  22:5189-5194. 2004
• INTERFACIAL BEHAVIOR IN TYPE IV SYSTEMS.  INTERNATIONAL JOURNAL OF THERMOPHYSICS.  25(5):1395-1414. 2004
• JOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY.  JOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY.  43:1895-1896. 2004
• CHEMICAL ENGINEERING SCIENCE.  CHEMICAL ENGINEERING SCIENCE.  58(12):2529-2550. 2003
• CHEMICAL ENGINEERING SCIENCE.  CHEMICAL ENGINEERING SCIENCE.  58(19):4363-4376. 2003
• ESTIMATION OF LIQUID-LIQUID-VAPOR EQUILIBRIA USING PREDICTIVE EOS MODELS. 1. CARBON DIOXIDE-N-ALKANES.  JOURNAL OF PHYSICAL CHEMISTRY B.  107:1864-1874. 2003
• ESTIMATION OF PHASE BEHAVIOR IN MIXTURES OF CO2 AND C20 + N-ALKANES USING PREDICTIVE OS MODELS.  PHYSICS AND CHEMISTRY OF LIQUIDS.  41:623-637. 2003
• ISOBARIC VAPOR-LIQUID EQUILIBRIA AND DENSITIES FOR THE BINARY SYSTEMS OXALANE + ETHYL 1,1-DIMETHYLETHYL ETHER, OXOLANE + 2-PROPANOL AND PROPAN-2-ONE + TRICHLOROMETHANE.  PHYSICS AND CHEMISTRY OF LIQUIDS.  41:283-301. 2003
• ISOBARIC VAPOR-LIQUID EQUILIBRIA FOR THE TERNARY SYSTEM OXOLANE + ETHYL 1,1-DIMETHYLETHYL ETHER + 2-PROPANOL AT 50 KPA.  PHYSICS AND CHEMISTRY OF LIQUIDS.  41:493-501. 2003
• JOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY.  JOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY.  42:5662-5673. 2003
• ABOUT THE RELATION BETWEEN THE EMPIRICAL AND THEORETICALLY BASED PARTS OF VAN DER WAALS-LIKE EQUATIONS OF STATE.  INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH.  41:4414-4421. 2002
• CANADIAN JOURNAL OF CHEMICAL ENGINEERING.  CANADIAN JOURNAL OF CHEMICAL ENGINEERING.  80:927-942. 2002
• CLOSED LOOPS OF LIQUID-LIQUID IMMISCIBILITY PREDICTED BY SEMI-EMPIRICAL CUBIC EQUATIONS OF STATE AND CLASSICAL MIXING RULES.  PHYSICAL CHEMISTRY CHEMICAL PHYSICS.  4:879-883. 2002
• COMMENTS ON "DEVELOPMENT OF A UNIVERSAL GROUP CONTRIBUTION EQUATION OF STATE. 2, PREDICTION OF VAPOR-LIQUID EQUILIBRIA FOR ASYMMETRIC SYSTEMS" BY JENS AHLERS AND JÜRGEN GMEHLING (IND. ENG. CHEM. RES. 2002, 41, 3489-3498).  INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH.  41:6634-6634. 2002
• ISOBARIC VAPOR-LIQUID EQUILIBRIA AND DENSITIES FOR THE SYSTEM ETHYL 1,1-DIMETHYLETHYL ETHER + 2-PROPANOL.  PHYSICS AND CHEMISTRY OF LIQUIDS.  40:685-702. 2002
• ISOBARIC VAPOR-LIQUID EQUILIBRIA AND DENSITIES FOR THE SYSTEM METHYL 1,1-DIMETHYLETHYL ETHER + 2-PROPANOL.  PHYSICS AND CHEMISTRY OF LIQUIDS.  40:277-294. 2002
• JOURNAL OF CHEMICAL AND ENGINEERING DATA.  JOURNAL OF CHEMICAL AND ENGINEERING DATA.  47:1256-1262. 2002
• PHASE EQUILIBRIA IN THE SYSTEMS 1-HEXENE + HEPTANE AND 1-HEXENE ´ETHYL 1,1-DIMETHYLETHYL ETHER + HEPTANE AT 94.00 KPA.  PHYSICS AND CHEMISTRY OF LIQUIDS.  40:277-281. 2002
• A MODEL-FREE APPROACH DATA TREATMENT OF VAPOR-LIQUID EQUILIBRIUM DATA IN TERNARY SYSTEMS. 1. THEORY AND NUMERICAL PROCEDURES.  JOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY.  40:2134-2148. 2001
• A MODEL-FREE APPROACH DATA TREATMENT OF VAPOR-LIQUID EQUILIBRIUM DATA IN TERNARY SYSTEMS. 2. APPLICATIONS.  JOURNAL OF INDUSTRIAL AND ENGINEERING CHEMISTRY.  40:2149-2159. 2001
• CHEMICAL ENGINEERING SCIENCE.  CHEMICAL ENGINEERING SCIENCE.  56(2):6485-6510. 2001
• FLUID PHASE EQUILIBRIA.  FLUID PHASE EQUILIBRIA.  166:141-162. 1999